JPH07173520A - Method for dephosphorizing chromium-containing molten iron and molten steel - Google Patents
Method for dephosphorizing chromium-containing molten iron and molten steelInfo
- Publication number
- JPH07173520A JPH07173520A JP31812593A JP31812593A JPH07173520A JP H07173520 A JPH07173520 A JP H07173520A JP 31812593 A JP31812593 A JP 31812593A JP 31812593 A JP31812593 A JP 31812593A JP H07173520 A JPH07173520 A JP H07173520A
- Authority
- JP
- Japan
- Prior art keywords
- chromium
- molten iron
- flux
- dephosphorizing
- dephosphorization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
Description
【0001】[0001]
【技術分野】本願発明は製銑および製鋼の操業におい
て、クロムを1%以上含む溶銑および溶鋼(以下溶鉄と
いう)の脱燐方法に関する。TECHNICAL FIELD The present invention relates to a method for dephosphorizing hot metal and molten steel (hereinafter referred to as molten iron) containing 1% or more of chromium in the operation of pig iron and steelmaking.
【0002】[0002]
【従来技術】溶鉄中の燐は、一般に鋼の品質にとって有
害な元素であり、その除去は製鋼技術上の重要な課題で
ある。一般に普通鋼においてはその技術はほぼ確立され
ているが、クロムを含む溶鉄においては、Cr2 O3 の
生成によるスラグの流動性の低下或はクロムによる燐の
活量の低下により、燐を所望のレベルまで経済的に低減
させることは、実操業上極めて困難な現状にある。従っ
て通常、燐含有量の低い原料を使用することによって低
燐溶鉄の製造に対処している。2. Description of the Related Art Phosphorus in molten iron is an element that is generally harmful to the quality of steel, and its removal is an important issue in steelmaking technology. Generally, in the case of ordinary steel, the technology is almost established, but in molten iron containing chromium, phosphorus is desired due to the decrease of fluidity of slag due to formation of Cr 2 O 3 or the decrease of phosphorus activity due to chromium. It is extremely difficult in actual operation to economically reduce to the level. Therefore, the production of low-phosphorus molten iron is usually dealt with by using a raw material having a low phosphorus content.
【0003】脱燐に及ぼす重要な因子は脱燐用フラック
スの組成および添加方法である。添加方法については、
昨今提案されている添加方法は、例えば特公平4−18
005号、特公平2−7363号および特開平1−20
5024号各公報に、AOD炉においてガス撹拌添加す
る方法およびAOD等の撹拌機能をもつ精練炉が提案さ
れている。An important factor affecting dephosphorization is the composition and addition method of the dephosphorization flux. For addition method,
The recently proposed addition method is, for example, Japanese Patent Publication No. 4-18.
No. 005, Japanese Patent Publication No. 2-7363 and Japanese Patent Laid-Open No. 1-20
No. 5024 each proposes a method of stirring and adding gas in an AOD furnace and a refining furnace having a stirring function such as AOD.
【0004】[0004]
【発明が解決しようとする課題】本願発明は、クロムを
1%以上含む溶銑および溶鋼の脱燐において、クロムの
酸化によるフラックスの流動性の低下を抑え、不経済な
原料の選別が不要で、費用のかかる特別な装置も使用せ
ず、かつO2 源として安価な電気炉集塵ダストを使用す
ることにより、実操業上で充分な効果の挙がる、効率が
良く安価な溶鉄の脱燐方法を提供することに関する。DISCLOSURE OF THE INVENTION In the present invention, in dephosphorization of molten pig iron and molten steel containing 1% or more of chromium, deterioration of flux fluidity due to oxidation of chromium is suppressed, and uneconomical selection of raw materials is unnecessary. A highly efficient and inexpensive molten iron dephosphorization method that has a sufficient effect in actual operation by using inexpensive electric furnace dust collection dust as an O 2 source without using any expensive special equipment. Regarding providing.
【0005】[0005]
【課題を解決するための手段】本願発明の特徴は脱燐用
フラックスの添加方法にある。すなわち溶解炉或は精練
炉より出湯しようとする取鍋内または出湯流ないしはそ
の落下位置近傍に投入し、出湯流による撹拌力を利用す
ることを特徴とする方法である。A feature of the present invention resides in a method of adding a flux for dephosphorization. That is, the method is characterized in that the molten metal is charged into the ladle to be tapped from the melting furnace or the refining furnace or to the tapping flow or the vicinity of the dropping position, and the stirring force by the tapping flow is used.
【0006】溶鉄の脱燐は下記の化学反応にてPをP2
O5 に変え、フラックス中のCaOで捕捉することによ
って行われる。For dephosphorization of molten iron, P is converted into P 2 by the following chemical reaction.
It is performed by changing to O 5 and capturing with CaO in the flux.
【0007】4[P]+5O2 →2(P2 O5 ) ここでO2 源としてはスケール等の固体酸素、或は気体
酸素が、フラックスとしてはCaO−CaF2 系、Ca
O−CaF2 −CaCO3 系、或はCaO−CaF2 −
CaCl2 系等の公知の各種フラックスが使用可能であ
るが、本願発明としては特に、O2 源として電気炉集塵
ダストを、使用する固体酸素の一部または全量置き換え
ることである。4 [P] + 5O 2 → 2 (P 2 O 5 ) Here, solid oxygen such as scale or gaseous oxygen is used as the O 2 source, and CaO--CaF 2 system, Ca is used as the flux.
O-CaF 2 -CaCO 3 system, or CaO-CaF 2 -
Although various known fluxes such as CaCl 2 type can be used, the present invention particularly replaces the electric furnace dust collection dust as the O 2 source with a part or all of the solid oxygen used.
【0008】周知のごとく電気炉集塵ダストはPd、C
d等の有害元素を含有するため、通常安定化処理後埋め
立て処分されているが、本願発明の方法で使用すること
によりFeの他有価金属の一部が回収され、産業廃棄物
の有効利用が計れる。As is well known, the dust collected in the electric furnace is Pd, C.
Since it contains harmful elements such as d, it is normally disposed of in landfill after stabilization treatment. However, by using the method of the present invention, a part of other valuable metals of Fe is recovered, and effective use of industrial waste is possible. Can be measured.
【0009】これらのフラックスは本願発明による溶鉄
への添加方法により、迅速に溶解し、滓化するとともに
流動性を保ち、溶鉄と充分混合してスラグ/メタル界面
反応が行われる。By the method of adding to the molten iron according to the present invention, these fluxes are rapidly dissolved, turned into slag and maintain fluidity, and are sufficiently mixed with molten iron to carry out the slag / metal interface reaction.
【0010】本願発明の添加方法における撹拌力は10
0〜300watt/tであり、AOD等の精練炉に比
べれば1/10以下であるが、比重の大きく異なるフラ
ックスと溶鉄の混合が充分行われるため、目的を達成す
ることが可能である。The stirring force in the addition method of the present invention is 10
It is 0 to 300 watt / t, which is 1/10 or less as compared with a refining furnace such as AOD. However, since the flux and the molten iron having greatly different specific gravities are sufficiently mixed, the object can be achieved.
【0011】一方、滓化したフラックスの流動性は下記
の反応式により生成するCr2 O3により著しく阻害さ
れる。On the other hand, the fluidity of the slag-like flux is significantly hindered by Cr 2 O 3 produced by the following reaction formula.
【0012】4Cr + 3O2 → 2Cr2 O3 この点が含クロム溶鉄における脱燐の困難さであり、少
なくともスラグ中のCr2 O3 濃度を10%以下、望ま
しくは5%以下に抑えることが必要である。上記のCr
2 O3 濃度に抑制するためには、脱燐処理温度の選定が
重要であり、下記のHiltyの経験式から計算される
温度(T)より高い温度で処理することにより達成され
る。4Cr + 3O 2 → 2Cr 2 O 3 This is the difficulty of dephosphorization in molten iron containing chromium, and it is possible to suppress the Cr 2 O 3 concentration in the slag to 10% or less, preferably 5% or less. is necessary. Cr above
In order to suppress the 2 O 3 concentration, the selection of the dephosphorization treatment temperature is important, and it can be achieved by treating at a temperature higher than the temperature (T) calculated from the following Hilty's empirical formula.
【0013】log([%Cr]/[%C])=−13
800/T+8.76 例えばC=4%、Cr=5%のとき、処理温度を限界温
度(T)=1593°K(1320℃)以上にすれば良
い。Log ([% Cr] / [% C]) =-13
800 / T + 8.76 For example, when C = 4% and Cr = 5%, the processing temperature may be set to the limit temperature (T) = 1593 ° K (1320 ° C) or higher.
【0014】上記の温度条件により、実施例で具体例を
説明するごとく、約5%以下のスラグ中のCr2 O3 濃
度および高い脱燐率が達成される。The above temperature conditions achieve a Cr 2 O 3 concentration in the slag of less than about 5% and a high dephosphorization rate, as will be illustrated in the examples.
【0015】[0015]
【効果】以上に述べたごとく、本願発明は、安価で効率
の良いクロム含有溶鉄の脱燐方法を提供するものであ
り、クロム含有溶鉄の品質向上に寄与する。[Effect] As described above, the present invention provides an inexpensive and efficient method for dephosphorizing molten iron containing chromium, which contributes to improving the quality of molten iron containing chromium.
【0016】また電気炉集塵ダストを使用することによ
り、フラックスのコストが安価になるばかりでなく、F
eの他有価金属の一部が回収され、産業廃棄物の量を減
ずることに寄与することになる。Further, by using the dust collected by the electric furnace, not only the cost of the flux becomes low, but also the F
e A part of other valuable metals is recovered, which contributes to reducing the amount of industrial waste.
【0017】[0017]
【実施例】実施例1 試験装置の配置を図1に示す。クロム含有溶鉄約2tを
低周波誘導炉1にて大気溶解し、温度を調整した後、脱
燐用フラックスとO2 源であるスケールを出湯しようと
する取鍋2内に入置、入置と出湯流近傍への添加の併用
の2通りの方法にて脱燐試験を実施した。EXAMPLES Example 1 The arrangement of the test equipment is shown in FIG. About 2 tons of molten iron containing chromium was melted in the low-frequency induction furnace 1 into the atmosphere, and after adjusting the temperature, the flux for dephosphorization and the scale as the O 2 source were placed and placed in the ladle 2 to be tapped. The dephosphorization test was carried out by two methods, in which the addition was made in the vicinity of the molten metal flow.
【0018】そのときの脱燐前溶鉄成分、フラックス原
単位、フラックス添加方法および処理温度を表1に示
す。Table 1 shows the molten iron component before dephosphorization, the flux basic unit, the flux addition method and the treatment temperature at that time.
【0019】[0019]
【表1】 処理はいずれもHiltyの経験式から計算される温度
(T)より高い温度で実施した。得られた脱燐率をスケ
ール原単位との関連において図2に示す。いずれも高い
脱燐率が得られた。なおスラグ中のCr2 O3 濃度は図
3に示すように低く、スラグの流動性は良好な結果が得
られた。[Table 1] All treatments were carried out at a temperature higher than the temperature (T) calculated from Hilty's empirical formula. The obtained dephosphorization rate is shown in FIG. 2 in relation to the scale unit. In each case, a high dephosphorization rate was obtained. The Cr 2 O 3 concentration in the slag was low as shown in FIG. 3, and the fluidity of the slag was good.
【0020】実施例2 実施例1における実験No.5と同一条件において、ス
ケールの約半量の50kg/tを普通鋼電気炉集塵ダス
トに置き換えた。その時の脱燐率は約85%と高いレベ
ルであった。 Example 2 Experiment No. 1 in Example 1 Under the same conditions as in No. 5, about half of the scale, 50 kg / t, was replaced with ordinary steel electric furnace dust collection dust. At that time, the dephosphorization rate was a high level of about 85%.
【図1】図1は脱燐処理における設備の配列をしめす模
式図である。FIG. 1 is a schematic diagram showing an arrangement of equipment for dephosphorization treatment.
【図2】図2はスケール原単位と脱燐率の関係を示した
図である。FIG. 2 is a diagram showing the relationship between the scale unit and the dephosphorization rate.
【図3】図3は各試験例におけるスラグ中のCr2 O3
濃度を示した図である。FIG. 3 shows Cr 2 O 3 in slag in each test example.
It is the figure which showed the density.
1 低周波誘導炉 2 取鍋 3 脱燐用フラックス 4 入置されたフラックス 5 出湯流に投入されたフラックス 6 フラックスホッパー 1 Low-frequency induction furnace 2 Ladle 3 Flux for dephosphorization 4 Flux that has been placed 5 Flux that has been added to the hot water flow 6 Flux hopper
Claims (2)
燐において、脱燐用フラックスを出湯しようとする取鍋
内または出湯流ないしはその落下位置近傍に投入する脱
燐方法であって、クロムの酸化によるフラックスの流動
性の低下を防ぐために、Hiltyの経験式、 log([%Cr]/[%C])=−13800/T+
8.76 から求められる炭素の優先酸化域の温度(T)以上の温
度で処理することを特徴とする方法。1. A dephosphorization method for dephosphorizing hot metal and molten steel containing 1% or more of chromium, in which a flux for dephosphorization is introduced into a ladle to be tapped, or near the pouring stream or its dropping position. Hilty's empirical formula: log ([% Cr] / [% C]) =-13800 / T +
8.76, wherein the treatment is performed at a temperature equal to or higher than the temperature (T) in the preferential oxidation region of carbon determined from 8.76.
を配合したフラックスを使用することを特徴とする請求
項1に記載の方法。2. The method according to claim 1, wherein a flux mixed with dust collected in an electric furnace is used as an oxygen source for the dephosphorization reaction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31812593A JPH07173520A (en) | 1993-12-17 | 1993-12-17 | Method for dephosphorizing chromium-containing molten iron and molten steel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31812593A JPH07173520A (en) | 1993-12-17 | 1993-12-17 | Method for dephosphorizing chromium-containing molten iron and molten steel |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07173520A true JPH07173520A (en) | 1995-07-11 |
Family
ID=18095788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31812593A Pending JPH07173520A (en) | 1993-12-17 | 1993-12-17 | Method for dephosphorizing chromium-containing molten iron and molten steel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07173520A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001073138A3 (en) * | 2000-03-24 | 2002-03-14 | Qual Chem Ltd | Steelmaking |
CN103194561A (en) * | 2013-04-03 | 2013-07-10 | 河北文丰钢铁有限公司 | Device for directly adding sintering returned dust into ladle |
KR20160063520A (en) | 2014-11-26 | 2016-06-07 | 주식회사 포스코 | Dephosporization method for chromium containing hot metal and method of manufacturing stainless steel |
-
1993
- 1993-12-17 JP JP31812593A patent/JPH07173520A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001073138A3 (en) * | 2000-03-24 | 2002-03-14 | Qual Chem Ltd | Steelmaking |
CN103194561A (en) * | 2013-04-03 | 2013-07-10 | 河北文丰钢铁有限公司 | Device for directly adding sintering returned dust into ladle |
KR20160063520A (en) | 2014-11-26 | 2016-06-07 | 주식회사 포스코 | Dephosporization method for chromium containing hot metal and method of manufacturing stainless steel |
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